CA1288022C - Continuous flow steam condensate removal device - Google Patents
Continuous flow steam condensate removal deviceInfo
- Publication number
- CA1288022C CA1288022C CA000565363A CA565363A CA1288022C CA 1288022 C CA1288022 C CA 1288022C CA 000565363 A CA000565363 A CA 000565363A CA 565363 A CA565363 A CA 565363A CA 1288022 C CA1288022 C CA 1288022C
- Authority
- CA
- Canada
- Prior art keywords
- passageway
- condensate
- unitary body
- downstream
- venturi
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0002—Casings; Housings; Frame constructions
- B01D46/0012—In-line filters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0002—Casings; Housings; Frame constructions
- B01D46/0017—Filter elements installed in a branch of a pipe, e.g. with an y-shaped tubular housing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/42—Auxiliary equipment or operation thereof
- B01D46/4227—Manipulating filters or filter elements, e.g. handles or extracting tools
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/42—Auxiliary equipment or operation thereof
- B01D46/4281—Venturi's or systems showing a venturi effect
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/66—Regeneration of the filtering material or filter elements inside the filter
- B01D46/70—Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter
- B01D46/72—Regeneration of the filtering material or filter elements inside the filter by acting counter-currently on the filtering surface, e.g. by flushing on the non-cake side of the filter with backwash arms, shoes or nozzles
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F16—ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
- F16T—STEAM TRAPS OR LIKE APPARATUS FOR DRAINING-OFF LIQUIDS FROM ENCLOSURES PREDOMINANTLY CONTAINING GASES OR VAPOURS
- F16T1/00—Steam traps or like apparatus for draining-off liquids from enclosures predominantly containing gases or vapours, e.g. gas lines, steam lines, containers
- F16T1/34—Steam traps or like apparatus for draining-off liquids from enclosures predominantly containing gases or vapours, e.g. gas lines, steam lines, containers without moving parts other than hand valves, e.g. labyrinth type
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T137/00—Fluid handling
- Y10T137/2931—Diverse fluid containing pressure systems
- Y10T137/3003—Fluid separating traps or vents
- Y10T137/3021—Discriminating outlet for liquid
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Nozzles (AREA)
Abstract
ABSTRACT
A continuous flow steam condensate removal device includes a Venturi-type nozzle of relatively small diameter formed in an intermediate portion of a unitary body. With respect to the Venturi-type nozzle, the unitary body includes an upstream annular conically tapered entrance surface, a relatively long condensate collection passageway for forming a condensate steam seal, and a flow-reduction passageway.
Downstream, the unitary body includes a condensate discharge-transition passageway and an enlarged-diameter frustoconical discharge passageway for flushing and maintaining a downstream condensate return line clear of debris.
A continuous flow steam condensate removal device includes a Venturi-type nozzle of relatively small diameter formed in an intermediate portion of a unitary body. With respect to the Venturi-type nozzle, the unitary body includes an upstream annular conically tapered entrance surface, a relatively long condensate collection passageway for forming a condensate steam seal, and a flow-reduction passageway.
Downstream, the unitary body includes a condensate discharge-transition passageway and an enlarged-diameter frustoconical discharge passageway for flushing and maintaining a downstream condensate return line clear of debris.
Description
1~8~
CONTINUOUS FLOW STEAM CONDENSATE REMOVAL DEVICE
This invention relates to a continuous flow steam condensate removal device, and more particularly to a Venturi-type steam condensate removal device of unitary construction which is less expensive and more efficient than prior known devices.
The use of devices or Usteam traps~ for the removal of condensate from steam lines is well known. In the past, mechanical devices which remain closed until a predetermined amount of condensate has collected therein, and periodically open to let the collected condensate pass through to a condensate receiving tank or reservoir, have been used. These devices, however, have a number of disadvantages, including initial high cost and high maintenance, repair and replacement costs. These traps also increase energy costs as a result of steam ~blowing through~ the relatively large open trap orifice, delays in the trap reclosing, or failure of the trap in an open .
. ,. ., -- . ~ ....... ... . . .. .. . .
- ~2~38C)Z2 condition so that the trap does not reclose at all. This ~blow through" also is disadvantageous because, the high temperature of the steam then tends to produce process temperature .
variations in associated equipment, causing reduced efficiency, and high temperatures and back pressure in the condensate receiving tank and its associated equipment.
Accordingly, more recently, Venturi-type devices of a continuous flow type have been used. For example, U.S. Patent No. 4,171,209, issued October 16, 1979, to Timothy S. Brown, discloses various Venturi-type devices (steam traps~ for removing condensate from steam lines, wherein the primary feature of each device is the provision of one or more screens in an upstream passageway of the device, to filter out debris which could cause clogging of a Venturi-type orifice extending through an intermediate portion of the device. Figures 8 and 9 of that patent disclose a device having a unitary body with external screw threads on both ends, a Venturi-type orifice in the center of the body, and long inlet and outlet passageways.
The device has a hexagonal form at its center and internal conical surfaces interconnecting the inlet and outlet passageways and the Venturi-type orifice. The unitary body is disclosed as being preferably formed of Type 304 stainless-steel. U.S. Patent Nos. 4,426,213 and 4,486,208, issuedJanuary 17 and December 4, 1984, respectively, to Constantine , .... . . . . . . . . . .
~880Z2 .. Sta~ropoulos, disclose similar devices having an insertable tubular nozzle structure in a unitary body.
It is therefore an object of the present in~ention t~
obviate or mitigate the above disad~antages by provi~ing a no~el continuous flow stea~ condensate removal device.
In general, this invention relates to a continuous flow steam condensate removal device comprising an elongated tubular unitary body having an entrance end, an intermediate portion and an exit end. A cylindrical Venturi-type nozzle of relatively small diameter is formed in the intermediate portion of the unitary body and extends along the longitudinal axis thereof. An elongated cylindrical upstream condensate collection passageway of larger diameter is formed in the unitary body and extends from adjacent the entrance end of the unitary body and along its longitudinal axis to adjacent the Venturi-type nozzle. Further, a conically-shaped downstream condensation discharge passageway in the unitary body extends along the longitudinal axis thereof and flares continuously outward in a downstream direction from adjacent the Venturi-type nozzle to substantially the exit end of the unitary body.
,, ,. . . , .. . _ .. ... -- . . , , ~." . . . . . . .
~28ao22 More speclfically, the steam condensate removal devioe oomprisesan elongated unitary body formed of No. 316 stainless steel, said body having e~ternal screw threads formed at opposite ends thereof, and said body having at least two opposite side flat surfaces formed intermediate said external screw-threads;
an elongated cylindrical upstream condensate collection passageway in said unitary body extending along a longitudinal axis of said unitary body;
an annular conically tapered surface surrounding an entrance to said elongated cylindrical upstream condensate collection passageway and extending inwardly in a downstream direction to facilitate flow into said condensate collection passageway;
a frustoconical downstream condensate discharge passageway in said unitary body flaring outward continuously in a downstream direction and extending along the longitudinal axis of said unitary body, said cylindrical upstream condensate collection passageway having a length on the order of at least twice that of said frustoconical downstream condensate discharge passageway, and said frustoconical downstream condensate discharge passageway having an initial upstream diameter larger than the diameter of said upstream condensation collection passageway;
. ..
~288022 `
a cylindrical Venturi-type nozzle in said unitary body snd estending along the longitudinal asis of said unitary body, said Venturi-type nozzle being located between said upstream condensate collection passaqeway and said downstream condensate discharge passageway and being of small diameter as compared to the diameters of said passageways;
upstream and downstream 10w-reduction and discharge-transition passageways in said unitary body and estending along the longitudinal asis of said unitary body between said upstream condensate collection passageway and said Venturi-type nozzle, and between said ~enturi-type nozzle and said frustoconical downstream condensate discharge passageway, respectively, said flow-reduction and discharge-transition passageways being of essentially the same diameter, said latter diameter being of a value intermediate the diameters of said upstream condensate collection passageway snd said venturi-type nozzle, and said frustoconical downstream condensate discharge passageway having a diameter on the order of at least double that of said condensate discharge transition passageway; and internal conically tapered surfaces in said unitary body interconnecting adjacent ones of said passageways and said Venturi-type nozzle.
-4a-~l288022 Embodiments of the present invention will now be des-cribed by ~ay of example only with reference to the accompanying drawings in which: -Figure 1 is a side view of a continuous flow steamcondensat:e removal device;
Figure 2 is a cross-sectional view taken along the center line of the device shown in Figure l; and Figure 3 is a partial cross-sectional view, showing another embodiment of a device in the accordance with the invention, mounted in a stèam condensate removal system.
Referring to Figure 1, a continuous flow steam condensate removal device 10 includes an elongated unitary body 12 having external screw threads 14 formed at its opposite ends. The unitary body 12 also has a he~agonal form, with opposite side flat surfaces 16, formed at its center intermediate the external screw threads 14, to facilitate connecting the device 10 with other screw threaded parts of a steam condensate removal system 18, as shown in Figure 3.
Referring to Figure 2, the unitary body 12 is formed with an elongated cylindrical upstream condensate collection passageway 20 extending along the longitudinal axis of the unitary body, and a frustoconical downstream condensate i 288~22 ~ischarge passageway `22 also e~tending along the longitudinal axis of the unitary body. A cylindrical Venturi-type nozzle or orifice 24 is formed in the unitary body 12 between the upstream condensate collection passageway 20 and the downstream condensate discharge passageway 22, and is of small diameter as compared to the diameters of the passageways.
An annular conically tapered surface 26 surrounds an entrance to the elongated cylindrical upstream condensate collection passageway 20 and extends inwardly in a downstream direction to facilitate flow into the condensate collection passageway. The upstream condensate collection passageway 20 is connected to an entrance end of the Venturi-type nozzle 24 by a flow-reduction passageway 28 of reduced diameter, and conically-shaped interconnecting surfaces 30. Similarly, an exit end of the Venturi-type nozzle 24 is connected with the downstream condensate discharge passageway 22 by a condensate discharge-transition passageway 32 of substantially the same diameter as the upstream condensate collection passageway, and conically-shaped interconnecting surfaces 34.
Figure 3 shows another embodiment of a continuous flow steam condensate removal device 10' which is similar to the device 10 shown in Figure 2, except for being smaller in overall size, and with respect to the internal dimensions of certain parts of the device. Otherwise, the device 10' shown .. . .. . . . ..... ..... . . .... ..
~X~38~Z~
in Figure 3 is identical to the device 10' shown in Figure 2, and corresponding parts of the device shown in Figure 3 are identified by the same reference numerals.
With further reference to Figure 3, the upstream end of the steam condensate removal device 10' is screw-threadably connected into one end of a device known as a Y-strainer 36.
The other end of the Y-strainer device 36 is screw-threadably connected to a steam line 38. A cylindrical screen 40 is disposed in a branch leg 42 of the Y-strainer device 36 so that steam and condensate flowing toward the steam condensate removal device 10' must pass through the screen for the removal of debris before the steam and condensate reach the steam condensate removal device. Preferably, the screen 40 is formed of perforated #60 mesh stainless steel, rather than a wire mesh screen, for greater rigidity, longer wear and less susceptibility to clogging. The branch leg 42 of the Y-strainer device 36 is provided with a blow-down valve 44 of a known type, for periodically removing dirt and other debris collected by the screen 40, in a known manner. The downstream end of the steam condensate removal device 10' is screw-threadably connected by a coupling member 46 to a condensate return line 48.
As is shown in Figure 3, in use of the steam condensate removal device 10', steam 46 attempts to pass ~288022 _hrough the Venturi-type nozzle 24' at a high velocity (approaching 760 MPH), while condensate 48 in the steam wants to travel through the Venturi-type nozzle at a much lower rate (e.g., 30 MPH). As a result, the condensate 48 tends to collect at the upstream end of the device 10' in the Y-strainer device 36 and in the condensate collection passageway 20' Accordingly, the condensate collection passageway 20' is of a relatively long length, such as on the order of twice that of the condensate discharge passageway 22 ', so that the condensate 48 collected therein can better function as a seal to prevent the escape of the steam 46 from the Y-strainer device 36 and the steam line 38, into the condensate return line 48. The reduced-diameter flow-reduction passageway 28' between the condensate collection passageway 20' and the Venturi-type nozzle 24' further enhances this sealing capability of the condensate 48.
As the condensate 48 collects in the condensate collection passageway 20' and in front of the entrance to the condensate collection passageway, as illustrated in Figure 3, the blocked steam 46 causes a pressure build-up in the collected condensate so that the condensate is periodically forced out of the condensate collection passageway, through the Venturi-type nozzle 24. The condensate 48 then travels through the discharge-transition passageway 22' and exits therefrom ~288022 through the frustoconical condensate discharge passageway 22' at high pressure in a fine spray 50, into the condensate return line 48, to cause a continuous flushing of debris through the coupli.ng member 46 and the return line, and preventing accum~lation of the debris therein.
To facilitate the discharge of the condensate 48 in the fine spray 50 and prevent the collection of debris in the coupling member 46 and the condensate return line 48, the frustoconical condensate discharge passageway 22' has a relatively large initial upstream diameter in comparison to the diameter of the condensate-discharge transition passageway 32'.
The frustoconical condensate discharge passageway 22' also flares outward continuously in a downstream direction for the same purpose, at a reduced angle to the longitudinal axis of the unitary one-piece body 12', as compared to an outwardly flaring angle of the adjacent interconnecting surface 34'.
Preferably, the initial upstream diameter of the condensate discharge passageway 22' also is larger than that of the condensate collection passageway 20' and at least double the diameter of the condensate discharge-transition passageway 32'.
The elongated unitary bodies 12 and 12' of the steam condensate removal devices 10 and 10' are preferably formed of a hard material, such as No. 316 stainless steel, so that the Venturi-type nozzles 24 and 24" have a long-wearing capability.
Forming the bodies 12 and 12' of this material Dj -`~
~288022 .lso produces devices 10 and 10' which have a pressure-withstanding capability of on the order of 2500 psig and a temperature-resistance capability of up to 3000F.
The steam condensate removal devices 10 and 10' are of different sizes, as noted previously, with selected internal dimensions being the same or different, depending on the size of-the steam line 38 and the expected degree of condensation therein. For example, the diameter of the Venturi-type nozzle 24 or 24' may vary from on the order of 0.024 inches to 0.554 inches, with other dimensions of the devices 10 and 10' modified accordingly. By way of illustration, the following table illustrates various dimensions of the different parts of the larger condensate removal device 10 shown in Figures 1 and 2, and the smaller condensate removal device 10' shown in Figure 3, respectively.
~288022 PARTFIGURES 1 and 2 FIGURE 3 .
(Inches) (Inches) Nozzle diameter .156 .105 Nozzle length .500 .S00 Condensate collection passageway diameter .375 .375 Discharge passageway .62S .375 initial diameter Discharge passageway .750 .5625 outer diameter Condensate collection 1.0 1.0 passageway length Discharge passageway .~00 .S00 length Flow-reduction .5625 .160 passageway length Flow-reduction .218 .150 passageway diameter Discharge-transition passageway length.125 .500 Discharge-transition.250 .150 passageway diameter iL28802X
In summary, a no~el ` steam condensate removal device, such as the devices 10 and 10', have been disclosed. The devices 10 and 10' are inexpensive to manufacture, and more efficient and long-wearing than prior known devices. The long condensate collection passageway 20 or 20' is desirable from the standpoint of preventing the escape of steam from the steam line 38 through the device 10 or 10' into the condensate return line 48. Further, the construction of the frustoconical condensate discharge passageway 22 or 22', wherein the passageway has an initial large diameter and flares continuously outward to the discharge end of the device, permits condensate to be expelled from the device in a fine spray 50 at high velocity, to reduce the collection of dirt and other debris in the couplin~ member 46 and the condensation return line 48.
Various other modifications, adaptations and alternative designs than those disclosed herein are, of course, possible in light of the above teachings. Therefore, it should be understood at this time that within the scope of the appended claims, the invention may be practiced otherwise than as specifically described herein.
CONTINUOUS FLOW STEAM CONDENSATE REMOVAL DEVICE
This invention relates to a continuous flow steam condensate removal device, and more particularly to a Venturi-type steam condensate removal device of unitary construction which is less expensive and more efficient than prior known devices.
The use of devices or Usteam traps~ for the removal of condensate from steam lines is well known. In the past, mechanical devices which remain closed until a predetermined amount of condensate has collected therein, and periodically open to let the collected condensate pass through to a condensate receiving tank or reservoir, have been used. These devices, however, have a number of disadvantages, including initial high cost and high maintenance, repair and replacement costs. These traps also increase energy costs as a result of steam ~blowing through~ the relatively large open trap orifice, delays in the trap reclosing, or failure of the trap in an open .
. ,. ., -- . ~ ....... ... . . .. .. . .
- ~2~38C)Z2 condition so that the trap does not reclose at all. This ~blow through" also is disadvantageous because, the high temperature of the steam then tends to produce process temperature .
variations in associated equipment, causing reduced efficiency, and high temperatures and back pressure in the condensate receiving tank and its associated equipment.
Accordingly, more recently, Venturi-type devices of a continuous flow type have been used. For example, U.S. Patent No. 4,171,209, issued October 16, 1979, to Timothy S. Brown, discloses various Venturi-type devices (steam traps~ for removing condensate from steam lines, wherein the primary feature of each device is the provision of one or more screens in an upstream passageway of the device, to filter out debris which could cause clogging of a Venturi-type orifice extending through an intermediate portion of the device. Figures 8 and 9 of that patent disclose a device having a unitary body with external screw threads on both ends, a Venturi-type orifice in the center of the body, and long inlet and outlet passageways.
The device has a hexagonal form at its center and internal conical surfaces interconnecting the inlet and outlet passageways and the Venturi-type orifice. The unitary body is disclosed as being preferably formed of Type 304 stainless-steel. U.S. Patent Nos. 4,426,213 and 4,486,208, issuedJanuary 17 and December 4, 1984, respectively, to Constantine , .... . . . . . . . . . .
~880Z2 .. Sta~ropoulos, disclose similar devices having an insertable tubular nozzle structure in a unitary body.
It is therefore an object of the present in~ention t~
obviate or mitigate the above disad~antages by provi~ing a no~el continuous flow stea~ condensate removal device.
In general, this invention relates to a continuous flow steam condensate removal device comprising an elongated tubular unitary body having an entrance end, an intermediate portion and an exit end. A cylindrical Venturi-type nozzle of relatively small diameter is formed in the intermediate portion of the unitary body and extends along the longitudinal axis thereof. An elongated cylindrical upstream condensate collection passageway of larger diameter is formed in the unitary body and extends from adjacent the entrance end of the unitary body and along its longitudinal axis to adjacent the Venturi-type nozzle. Further, a conically-shaped downstream condensation discharge passageway in the unitary body extends along the longitudinal axis thereof and flares continuously outward in a downstream direction from adjacent the Venturi-type nozzle to substantially the exit end of the unitary body.
,, ,. . . , .. . _ .. ... -- . . , , ~." . . . . . . .
~28ao22 More speclfically, the steam condensate removal devioe oomprisesan elongated unitary body formed of No. 316 stainless steel, said body having e~ternal screw threads formed at opposite ends thereof, and said body having at least two opposite side flat surfaces formed intermediate said external screw-threads;
an elongated cylindrical upstream condensate collection passageway in said unitary body extending along a longitudinal axis of said unitary body;
an annular conically tapered surface surrounding an entrance to said elongated cylindrical upstream condensate collection passageway and extending inwardly in a downstream direction to facilitate flow into said condensate collection passageway;
a frustoconical downstream condensate discharge passageway in said unitary body flaring outward continuously in a downstream direction and extending along the longitudinal axis of said unitary body, said cylindrical upstream condensate collection passageway having a length on the order of at least twice that of said frustoconical downstream condensate discharge passageway, and said frustoconical downstream condensate discharge passageway having an initial upstream diameter larger than the diameter of said upstream condensation collection passageway;
. ..
~288022 `
a cylindrical Venturi-type nozzle in said unitary body snd estending along the longitudinal asis of said unitary body, said Venturi-type nozzle being located between said upstream condensate collection passaqeway and said downstream condensate discharge passageway and being of small diameter as compared to the diameters of said passageways;
upstream and downstream 10w-reduction and discharge-transition passageways in said unitary body and estending along the longitudinal asis of said unitary body between said upstream condensate collection passageway and said Venturi-type nozzle, and between said ~enturi-type nozzle and said frustoconical downstream condensate discharge passageway, respectively, said flow-reduction and discharge-transition passageways being of essentially the same diameter, said latter diameter being of a value intermediate the diameters of said upstream condensate collection passageway snd said venturi-type nozzle, and said frustoconical downstream condensate discharge passageway having a diameter on the order of at least double that of said condensate discharge transition passageway; and internal conically tapered surfaces in said unitary body interconnecting adjacent ones of said passageways and said Venturi-type nozzle.
-4a-~l288022 Embodiments of the present invention will now be des-cribed by ~ay of example only with reference to the accompanying drawings in which: -Figure 1 is a side view of a continuous flow steamcondensat:e removal device;
Figure 2 is a cross-sectional view taken along the center line of the device shown in Figure l; and Figure 3 is a partial cross-sectional view, showing another embodiment of a device in the accordance with the invention, mounted in a stèam condensate removal system.
Referring to Figure 1, a continuous flow steam condensate removal device 10 includes an elongated unitary body 12 having external screw threads 14 formed at its opposite ends. The unitary body 12 also has a he~agonal form, with opposite side flat surfaces 16, formed at its center intermediate the external screw threads 14, to facilitate connecting the device 10 with other screw threaded parts of a steam condensate removal system 18, as shown in Figure 3.
Referring to Figure 2, the unitary body 12 is formed with an elongated cylindrical upstream condensate collection passageway 20 extending along the longitudinal axis of the unitary body, and a frustoconical downstream condensate i 288~22 ~ischarge passageway `22 also e~tending along the longitudinal axis of the unitary body. A cylindrical Venturi-type nozzle or orifice 24 is formed in the unitary body 12 between the upstream condensate collection passageway 20 and the downstream condensate discharge passageway 22, and is of small diameter as compared to the diameters of the passageways.
An annular conically tapered surface 26 surrounds an entrance to the elongated cylindrical upstream condensate collection passageway 20 and extends inwardly in a downstream direction to facilitate flow into the condensate collection passageway. The upstream condensate collection passageway 20 is connected to an entrance end of the Venturi-type nozzle 24 by a flow-reduction passageway 28 of reduced diameter, and conically-shaped interconnecting surfaces 30. Similarly, an exit end of the Venturi-type nozzle 24 is connected with the downstream condensate discharge passageway 22 by a condensate discharge-transition passageway 32 of substantially the same diameter as the upstream condensate collection passageway, and conically-shaped interconnecting surfaces 34.
Figure 3 shows another embodiment of a continuous flow steam condensate removal device 10' which is similar to the device 10 shown in Figure 2, except for being smaller in overall size, and with respect to the internal dimensions of certain parts of the device. Otherwise, the device 10' shown .. . .. . . . ..... ..... . . .... ..
~X~38~Z~
in Figure 3 is identical to the device 10' shown in Figure 2, and corresponding parts of the device shown in Figure 3 are identified by the same reference numerals.
With further reference to Figure 3, the upstream end of the steam condensate removal device 10' is screw-threadably connected into one end of a device known as a Y-strainer 36.
The other end of the Y-strainer device 36 is screw-threadably connected to a steam line 38. A cylindrical screen 40 is disposed in a branch leg 42 of the Y-strainer device 36 so that steam and condensate flowing toward the steam condensate removal device 10' must pass through the screen for the removal of debris before the steam and condensate reach the steam condensate removal device. Preferably, the screen 40 is formed of perforated #60 mesh stainless steel, rather than a wire mesh screen, for greater rigidity, longer wear and less susceptibility to clogging. The branch leg 42 of the Y-strainer device 36 is provided with a blow-down valve 44 of a known type, for periodically removing dirt and other debris collected by the screen 40, in a known manner. The downstream end of the steam condensate removal device 10' is screw-threadably connected by a coupling member 46 to a condensate return line 48.
As is shown in Figure 3, in use of the steam condensate removal device 10', steam 46 attempts to pass ~288022 _hrough the Venturi-type nozzle 24' at a high velocity (approaching 760 MPH), while condensate 48 in the steam wants to travel through the Venturi-type nozzle at a much lower rate (e.g., 30 MPH). As a result, the condensate 48 tends to collect at the upstream end of the device 10' in the Y-strainer device 36 and in the condensate collection passageway 20' Accordingly, the condensate collection passageway 20' is of a relatively long length, such as on the order of twice that of the condensate discharge passageway 22 ', so that the condensate 48 collected therein can better function as a seal to prevent the escape of the steam 46 from the Y-strainer device 36 and the steam line 38, into the condensate return line 48. The reduced-diameter flow-reduction passageway 28' between the condensate collection passageway 20' and the Venturi-type nozzle 24' further enhances this sealing capability of the condensate 48.
As the condensate 48 collects in the condensate collection passageway 20' and in front of the entrance to the condensate collection passageway, as illustrated in Figure 3, the blocked steam 46 causes a pressure build-up in the collected condensate so that the condensate is periodically forced out of the condensate collection passageway, through the Venturi-type nozzle 24. The condensate 48 then travels through the discharge-transition passageway 22' and exits therefrom ~288022 through the frustoconical condensate discharge passageway 22' at high pressure in a fine spray 50, into the condensate return line 48, to cause a continuous flushing of debris through the coupli.ng member 46 and the return line, and preventing accum~lation of the debris therein.
To facilitate the discharge of the condensate 48 in the fine spray 50 and prevent the collection of debris in the coupling member 46 and the condensate return line 48, the frustoconical condensate discharge passageway 22' has a relatively large initial upstream diameter in comparison to the diameter of the condensate-discharge transition passageway 32'.
The frustoconical condensate discharge passageway 22' also flares outward continuously in a downstream direction for the same purpose, at a reduced angle to the longitudinal axis of the unitary one-piece body 12', as compared to an outwardly flaring angle of the adjacent interconnecting surface 34'.
Preferably, the initial upstream diameter of the condensate discharge passageway 22' also is larger than that of the condensate collection passageway 20' and at least double the diameter of the condensate discharge-transition passageway 32'.
The elongated unitary bodies 12 and 12' of the steam condensate removal devices 10 and 10' are preferably formed of a hard material, such as No. 316 stainless steel, so that the Venturi-type nozzles 24 and 24" have a long-wearing capability.
Forming the bodies 12 and 12' of this material Dj -`~
~288022 .lso produces devices 10 and 10' which have a pressure-withstanding capability of on the order of 2500 psig and a temperature-resistance capability of up to 3000F.
The steam condensate removal devices 10 and 10' are of different sizes, as noted previously, with selected internal dimensions being the same or different, depending on the size of-the steam line 38 and the expected degree of condensation therein. For example, the diameter of the Venturi-type nozzle 24 or 24' may vary from on the order of 0.024 inches to 0.554 inches, with other dimensions of the devices 10 and 10' modified accordingly. By way of illustration, the following table illustrates various dimensions of the different parts of the larger condensate removal device 10 shown in Figures 1 and 2, and the smaller condensate removal device 10' shown in Figure 3, respectively.
~288022 PARTFIGURES 1 and 2 FIGURE 3 .
(Inches) (Inches) Nozzle diameter .156 .105 Nozzle length .500 .S00 Condensate collection passageway diameter .375 .375 Discharge passageway .62S .375 initial diameter Discharge passageway .750 .5625 outer diameter Condensate collection 1.0 1.0 passageway length Discharge passageway .~00 .S00 length Flow-reduction .5625 .160 passageway length Flow-reduction .218 .150 passageway diameter Discharge-transition passageway length.125 .500 Discharge-transition.250 .150 passageway diameter iL28802X
In summary, a no~el ` steam condensate removal device, such as the devices 10 and 10', have been disclosed. The devices 10 and 10' are inexpensive to manufacture, and more efficient and long-wearing than prior known devices. The long condensate collection passageway 20 or 20' is desirable from the standpoint of preventing the escape of steam from the steam line 38 through the device 10 or 10' into the condensate return line 48. Further, the construction of the frustoconical condensate discharge passageway 22 or 22', wherein the passageway has an initial large diameter and flares continuously outward to the discharge end of the device, permits condensate to be expelled from the device in a fine spray 50 at high velocity, to reduce the collection of dirt and other debris in the couplin~ member 46 and the condensation return line 48.
Various other modifications, adaptations and alternative designs than those disclosed herein are, of course, possible in light of the above teachings. Therefore, it should be understood at this time that within the scope of the appended claims, the invention may be practiced otherwise than as specifically described herein.
Claims (15)
1. A continuous flow steam condensate removal device, comprising:
an elongated tubular unitary body having an entrance end, an intermediate portion and an exit end;
a cylindrical Venturi-type nozzle of relatively small diameter in the intermediate portion of said unitary body and extending along the longitudinal axis thereof;
an elongated cylindrical upstream condensate collection passageway of larger diameter in said unitary body, said upstream condensate collection passageway extending from adjacent the entrance end of said unitary body and along the longitudinal axis of said unitary body to adjacent said Venturi-type nozzle; and a conically-shaped downstream condensate discharge passageway in said unitary body extending along the longitudinal axis of said unitary body and flaring continuously outward in a downstream direction from adjacent said Venturi-type nozzle to substantially the exit end of said unitary body.
an elongated tubular unitary body having an entrance end, an intermediate portion and an exit end;
a cylindrical Venturi-type nozzle of relatively small diameter in the intermediate portion of said unitary body and extending along the longitudinal axis thereof;
an elongated cylindrical upstream condensate collection passageway of larger diameter in said unitary body, said upstream condensate collection passageway extending from adjacent the entrance end of said unitary body and along the longitudinal axis of said unitary body to adjacent said Venturi-type nozzle; and a conically-shaped downstream condensate discharge passageway in said unitary body extending along the longitudinal axis of said unitary body and flaring continuously outward in a downstream direction from adjacent said Venturi-type nozzle to substantially the exit end of said unitary body.
2. The steam condensate removal device as recited in claim 1, wherein:
said cylindrical upstream condensate collection passageway has a length on the order of twice that of said conically-shaped downstream condensate discharge passageway.
said cylindrical upstream condensate collection passageway has a length on the order of twice that of said conically-shaped downstream condensate discharge passageway.
3. The steam condensate removal device as recited in claim 2, wherein:
said conically-shaped downstream condensate discharge passageway has an initial upstream diameter larger than the diameter of said upstream condensate collection passageway. .
said conically-shaped downstream condensate discharge passageway has an initial upstream diameter larger than the diameter of said upstream condensate collection passageway. .
4. The steam condensate removal device as recited in claim 1, wherein:
a downstream cylindrical condensate discharge-transition passageway in said unitary body extends along the longitudinal axis of the unitary body between the Venturi-type nozzle and the conically-shaped downstream condensate discharge passageway; and said conically-shaped downstream condensate discharge passageway has an initial upstream diameter more than double that of the diameter of said condensate discharge-transition passageway.
a downstream cylindrical condensate discharge-transition passageway in said unitary body extends along the longitudinal axis of the unitary body between the Venturi-type nozzle and the conically-shaped downstream condensate discharge passageway; and said conically-shaped downstream condensate discharge passageway has an initial upstream diameter more than double that of the diameter of said condensate discharge-transition passageway.
5. The steam condensate removal device as recited in claim 1, further comprising:
an annular conically tapered surface at the entrance end of said unitary body and surrounding an entrance to said elongated cylindrical upstream condensate collection passageway, said tapered surface egtending inwardly in a downstream direction to facilitate smooth flow into said condensate collection passageway.
an annular conically tapered surface at the entrance end of said unitary body and surrounding an entrance to said elongated cylindrical upstream condensate collection passageway, said tapered surface egtending inwardly in a downstream direction to facilitate smooth flow into said condensate collection passageway.
6. The steam condensate removal device as recited in claim 1, further comprising:
an upstream cylindrical flow-reduction passageway in said unitary body and extending along the longitudinal axis of said unitary body between the upstream condensate collection passageway and the Venturi-type nozzle;
a downstream cylindrical condensate discharge-transition passageway in said unitary body and extending along the longitudinal axis of said unitary body between the Venturi-type nozzle and the conically-shaped downstream condensate discharge passageway; and said flow-reduction passageway being of an intermediate diameter as compared to the diameters of said condensate collection passageway and said Venturi-type nozzle, and said condensate discharge-transition passageway being of an intermediate diameter as compared to said Venturi-type nozzle ?nd an initial diameter of said conically-shaped condensate discharge passageway.
an upstream cylindrical flow-reduction passageway in said unitary body and extending along the longitudinal axis of said unitary body between the upstream condensate collection passageway and the Venturi-type nozzle;
a downstream cylindrical condensate discharge-transition passageway in said unitary body and extending along the longitudinal axis of said unitary body between the Venturi-type nozzle and the conically-shaped downstream condensate discharge passageway; and said flow-reduction passageway being of an intermediate diameter as compared to the diameters of said condensate collection passageway and said Venturi-type nozzle, and said condensate discharge-transition passageway being of an intermediate diameter as compared to said Venturi-type nozzle ?nd an initial diameter of said conically-shaped condensate discharge passageway.
7. The steam condensate removal device as recited in claim 6, further comprising:
internal conically tapered surfaces in said unitary body interconnecting adjacent ones of said passageways and said Venturi-type nozzle.
internal conically tapered surfaces in said unitary body interconnecting adjacent ones of said passageways and said Venturi-type nozzle.
8. The steam condensate removal device as recited in claim 6, wherein:
said cylindrical upstream condensate collection passageway has a length on the order of twice that of said conically-shaped downstream condensate discharge passageway.
said cylindrical upstream condensate collection passageway has a length on the order of twice that of said conically-shaped downstream condensate discharge passageway.
9. The steam condensate removal device as recited in claim 8, wherein:
said conically-shaped downstream condensate discharge passageway has an initial upstream diameter more than double that of the diameter of said condensate discharge-transition passageway.
said conically-shaped downstream condensate discharge passageway has an initial upstream diameter more than double that of the diameter of said condensate discharge-transition passageway.
10. The steam condensate removal device as recited in claim 7, wherein:
said elongated unitary body is formed of No. 316 stainless steel, and said body has external screw threads formed at opposite ends thereof and has at least two opposite side flat surfaces formed intermediate said external screw threads.
said elongated unitary body is formed of No. 316 stainless steel, and said body has external screw threads formed at opposite ends thereof and has at least two opposite side flat surfaces formed intermediate said external screw threads.
11. A continuous flow steam condensate removal device, comprising:
an elongated unitary body formed of No. 316 stainless steel, said body having external screw threads formed at opposite ends thereof, and said body having at least two opposite side flat surfaces formed intermediate said external screw-threads;
an elongated cylindrical upstream condensate collection passageway in said unitary body extending along a longitudinal axis of said unitary body;
an annular conically tapered surface surrounding an entrance to said elongated cylindrical upstream condensate collection passageway and extending inwardly in a downstream direction to facilitate flow into said condensate collection passageway;
a frustoconical downstream condensate discharge passageway in said unitary body flaring outward continuously in a downstream direction and extending along the longitudinal axis of said unitary body, said cylindrical upstream condensate collection passageway having a length on the order of at least twice that of said frustoconical downstream condensate discharge passageway, and said frustoconical downstream condensate discharge passageway having an initial upstream diameter larger than the diameter of said upstream condensation collection passageway;
a cylindrical Venturi-type nozzle in said unitary body and extending along the longitudinal axis of said unitary body, said Venturi-type nozzle being located between said upstream condensate collection passageway and said downstream condensate discharge passageway and being of small diameter as compared to the diameters of said passageways;
upstream and downstream flow-reduction and discharge-transition passageways in said unitary body and extending along the longitudinal axis of said unitary body between said upstream condensate collection passageway and said Venturi-type nozzle, and between said Venturi-type nozzle and said frustoconical downstream condensate discharge passageway, respectively, said flow-reduction and discharge-transition passageways being of essentially the same diameter, said latter diameter being of a value intermediate the diameters of said upstream condensate collection passageway and said Venturi-type nozzle, and said frustoconical downstream condensate discharge passaeway having a diameter on the order of at least double that of said condensate discharge transition passageway; and internal conically tapered surfaces in said unitary body interconnecting adjacent ones of said passageways and said Venturi-type nozzle.
an elongated unitary body formed of No. 316 stainless steel, said body having external screw threads formed at opposite ends thereof, and said body having at least two opposite side flat surfaces formed intermediate said external screw-threads;
an elongated cylindrical upstream condensate collection passageway in said unitary body extending along a longitudinal axis of said unitary body;
an annular conically tapered surface surrounding an entrance to said elongated cylindrical upstream condensate collection passageway and extending inwardly in a downstream direction to facilitate flow into said condensate collection passageway;
a frustoconical downstream condensate discharge passageway in said unitary body flaring outward continuously in a downstream direction and extending along the longitudinal axis of said unitary body, said cylindrical upstream condensate collection passageway having a length on the order of at least twice that of said frustoconical downstream condensate discharge passageway, and said frustoconical downstream condensate discharge passageway having an initial upstream diameter larger than the diameter of said upstream condensation collection passageway;
a cylindrical Venturi-type nozzle in said unitary body and extending along the longitudinal axis of said unitary body, said Venturi-type nozzle being located between said upstream condensate collection passageway and said downstream condensate discharge passageway and being of small diameter as compared to the diameters of said passageways;
upstream and downstream flow-reduction and discharge-transition passageways in said unitary body and extending along the longitudinal axis of said unitary body between said upstream condensate collection passageway and said Venturi-type nozzle, and between said Venturi-type nozzle and said frustoconical downstream condensate discharge passageway, respectively, said flow-reduction and discharge-transition passageways being of essentially the same diameter, said latter diameter being of a value intermediate the diameters of said upstream condensate collection passageway and said Venturi-type nozzle, and said frustoconical downstream condensate discharge passaeway having a diameter on the order of at least double that of said condensate discharge transition passageway; and internal conically tapered surfaces in said unitary body interconnecting adjacent ones of said passageways and said Venturi-type nozzle.
12. The steam condensate removal device as recited in claim 11, wherein:
said cylindrical upstream condensate collection passageway is on the order of twice the length of said frustoconical downstream condensate discharge passageway.
said cylindrical upstream condensate collection passageway is on the order of twice the length of said frustoconical downstream condensate discharge passageway.
13. The steam condensate removal device as recited in claim 1, which further comprises:
a downstream cylindrical condensate discharge-transition passageway of larger diameter than said Venturi-type nozzle in said unitary body and extending along the longitudinal axis of said unitary body from adjacent said Venturi-type nozzle; and a conically-shaped internal portion in said unitary body and interconnecting an exit end of said downstream cylindrical condensate discharge-transition passageway and said conically-shaped downstream condensate discharge passageway, said conically-shaped interconnecting portion and said conically-shaped downstream condensate discharge passageway flaring outward at different respective angles to the longitudinal axis of said unitary body.
a downstream cylindrical condensate discharge-transition passageway of larger diameter than said Venturi-type nozzle in said unitary body and extending along the longitudinal axis of said unitary body from adjacent said Venturi-type nozzle; and a conically-shaped internal portion in said unitary body and interconnecting an exit end of said downstream cylindrical condensate discharge-transition passageway and said conically-shaped downstream condensate discharge passageway, said conically-shaped interconnecting portion and said conically-shaped downstream condensate discharge passageway flaring outward at different respective angles to the longitudinal axis of said unitary body.
14. The steam condensate removal device as recited in claim 13, wherein said downstream conically-shaped condensate discharge passageway flares outward at a reduced angle with respect to said conically-shaped interconnecting portion.--
15. The steam condensate removal device as recited in claim 13, wherein said downstream cylindrical condensate discharge-transition passageway is of an intermediate diameter as compared to the diameter of said upstream condensate collection passageway and said Venturi-type nozzle.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US043,601 | 1987-04-28 | ||
| US07/043,601 US4745943A (en) | 1987-04-28 | 1987-04-28 | Continuous flow steam condensate removal device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1288022C true CA1288022C (en) | 1991-08-27 |
Family
ID=21927994
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000565363A Expired - Lifetime CA1288022C (en) | 1987-04-28 | 1988-04-28 | Continuous flow steam condensate removal device |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US4745943A (en) |
| CA (1) | CA1288022C (en) |
Families Citing this family (33)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5120336A (en) * | 1988-09-12 | 1992-06-09 | Leblanc Thomas F | Flow constriction device in radiator steam trap |
| US5123452A (en) * | 1988-09-12 | 1992-06-23 | Leblanc Thomas F | Flow constriction device for removal of condensate |
| US5060686A (en) * | 1989-12-27 | 1991-10-29 | Engineering Resources, Inc. | Multi-piece nozzle for steam condensate removal devices |
| US5088518A (en) * | 1991-02-28 | 1992-02-18 | Steam Tech, Inc. | Steam restricter device |
| US5137556A (en) * | 1991-06-11 | 1992-08-11 | Accu-Flow Tech, Inc. | Steam condensate drainage device for a steam piping system |
| US5429150A (en) * | 1994-02-17 | 1995-07-04 | Siefers, Jr.; H. Kenneth | Continuous flow steam condensate removal device |
| US5948128A (en) * | 1995-05-16 | 1999-09-07 | Engineering Resources, Inc. | Flanged condensate removal system with removable insert |
| US6148844A (en) * | 1998-07-01 | 2000-11-21 | Steam Tech, Inc. | Condensate removal device |
| US7261713B2 (en) | 2001-10-09 | 2007-08-28 | Synthes (Usa) | Adjustable fixator |
| GB0704633D0 (en) * | 2007-03-09 | 2007-04-18 | Spirax Sarco Ltd | A float operated mechanism |
| US20090044868A1 (en) * | 2007-08-14 | 2009-02-19 | Ying Chuan Chiang | Steam trap with capillary action based blocking arrangement |
| US20090044867A1 (en) * | 2007-08-14 | 2009-02-19 | Ying Chuan Chiang | Mechanism for facilitating cleaning of filter of steam trap without shutting down boiler |
| CN102762698B (en) * | 2010-02-18 | 2014-10-22 | 国际壳牌研究有限公司 | Tubular wall assembly and gasification reactor |
| GB2478536B (en) * | 2010-03-08 | 2012-06-20 | Gardner Energy Man Ltd | Condensate removal device |
| US20120125867A1 (en) * | 2010-11-24 | 2012-05-24 | Delaware Capital Formation, Inc. | Flushable filter device |
| CA2784238A1 (en) * | 2012-07-27 | 2014-01-27 | Jay R. Morris | Method of increasing efficiency of a y strainer and a y strainer |
| GB201304935D0 (en) * | 2013-03-18 | 2013-05-01 | Thermal Energy Internat Uk Ltd | Condensate removal device |
| US9896909B2 (en) | 2013-05-15 | 2018-02-20 | Halliburton Energy Services, Inc. | Downhole adjustable steam injection mandrel |
| CN105518373B (en) | 2013-08-02 | 2018-09-28 | 環保冠有限公司 | Nozzle-type drain valve |
| JP6086457B2 (en) * | 2015-03-13 | 2017-03-01 | 株式会社ボイラエンジニアリング | Strainer cleaning device |
| JP5833266B1 (en) * | 2015-04-17 | 2015-12-16 | 株式会社エコファースト | Nozzle for steam trap |
| JP5794653B1 (en) * | 2015-05-27 | 2015-10-14 | 命得 金城 | steam trap |
| KR101589040B1 (en) * | 2015-06-25 | 2016-01-27 | 최병화 | Pump system and its controling method for cleaning strainer |
| KR20170064222A (en) * | 2015-12-01 | 2017-06-09 | 티에스케이 주식회사 | Bellows-type Steam Trap |
| CA2916272A1 (en) * | 2015-12-23 | 2017-06-23 | Jay R. Morris | High pressure sand trap with screen |
| WO2017175744A1 (en) | 2016-04-04 | 2017-10-12 | 株式会社エコファースト | Nozzle-type steam trap |
| WO2018063990A1 (en) * | 2016-09-27 | 2018-04-05 | Equistar Chemicals, Lp | Strainers, methods, and filter assemblies therefor with improved sealing |
| JP6531310B1 (en) * | 2018-04-17 | 2019-06-19 | 株式会社エコファースト | Monitoring system |
| GB201807836D0 (en) | 2018-05-15 | 2018-06-27 | Thermal Energy International Uk Ltd | Condensate removal device |
| GB201812292D0 (en) | 2018-07-27 | 2018-09-12 | Thermal Energy International Uk Ltd | Cleaning device for condensate removal device |
| US11035570B2 (en) * | 2018-08-14 | 2021-06-15 | Airgas, Inc. | Method for removing large amounts of condensate from an underground vault steam system during startup |
| USD1018799S1 (en) * | 2022-07-30 | 2024-03-19 | Steamgard, Llc | Nozzle cartridge for steam trap |
| US11788684B1 (en) * | 2022-10-08 | 2023-10-17 | Steamgard, Llc | Steam trap construction with ease of access for maintenance |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2790463A (en) * | 1956-03-19 | 1957-04-30 | Delano & Garner Mfg Co | Flow regulator |
| US4171209A (en) * | 1977-02-07 | 1979-10-16 | Thermal Con-Serv Corp. | Apparatus for removing condensate from steam lines, and the like |
| US4486208A (en) * | 1980-11-17 | 1984-12-04 | Engineering Resources, Inc. | Condensate removal device for steam lines and the like |
| US4426213A (en) * | 1980-11-17 | 1984-01-17 | Engineering Resources, Inc. | Condensate removal device for steam lines and the like |
-
1987
- 1987-04-28 US US07/043,601 patent/US4745943A/en not_active Expired - Fee Related
-
1988
- 1988-04-28 CA CA000565363A patent/CA1288022C/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| US4745943A (en) | 1988-05-24 |
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